- InChI
- InChI=1S/C16H34/c1-3-5-7-9-11-13-15-16-14-12-10-8-6-4-2/h3-16H2,1-2H3
- InChI Key
- DCAYPVUWAIABOU-UHFFFAOYSA-N
- Formula
- C16H34
- SMILES
- CCCCCCCCCCCCCCCC
- Molecular Weight1
- 226.44
- CAS
- 544-76-3
- Other Names
-
- CETANE
- N-CETANE
- n-Hexadecane
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Tfus : Melting point (K).
- Vc : Critical Volume (m3/kmol).
- vspec : Specific Volume (m3/kg).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7420 | KDB | |
| ΔcH°liquid | [-10699.10; -10699.10] | kJ/mol |
|
| ΔcH°liquid | -10699.10 ± 1.80 | kJ/mol | NIST |
| ΔcH°liquid | -10699.10 ± 4.10 | kJ/mol | NIST |
| ΔfG° | 83.74 | kJ/mol | KDB |
| Rg | 8.3180 | KDB | |
| ΔfH°gas | [-374.90; -373.60] | kJ/mol |
|
| ΔfH°gas | -373.60 | kJ/mol | KDB |
| ΔfH°gas | -374.90 | kJ/mol | NIST |
| ΔfH°gas | -374.70 | kJ/mol | NIST |
| ΔfH°liquid | [-456.30; -456.10] | kJ/mol |
|
| ΔfH°liquid | -456.30 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -456.10 ± 4.10 | kJ/mol | NIST |
| ΔfusH° | 50.04 | kJ/mol | Silver ... |
| ΔsubH° | 135.10 | kJ/mol | NIST |
| ΔvapH° | [80.60; 81.80] | kJ/mol |
|
| ΔvapH° | 81.38 | kJ/mol | NIST |
| ΔvapH° | 81.80 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 81.40 | kJ/mol | NIST |
| ΔvapH° | 81.40 | kJ/mol | NIST |
| ΔvapH° | 81.20 | kJ/mol | NIST |
| ΔvapH° | 81.40 | kJ/mol | NIST |
| ΔvapH° | 81.40 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 81.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 80.60 ± 1.50 | kJ/mol | NIST |
| log10WS | [-8.40; -8.40] |
|
|
| log10WS | -8.40 | Aq. Sol... | |
| log10WS | -8.40 | Estimat... | |
| logPoct/wat | 6.488 | Crippen Calculated Property | |
| McVol | 236.300 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| Pc | [1400.00; 1401.00] | kPa |
|
| Pc | 1400.00 | kPa | KDB |
| Pc | 1400.00 ± 200.00 | kPa | NIST |
| Pc | 1401.00 ± 50.00 | kPa | NIST |
| ρc | [218.97; 226.44] | kg/m3 |
|
| ρc | 226.44 ± 45.29 | kg/m3 | NIST |
| ρc | 218.97 ± 6.79 | kg/m3 | NIST |
| Inp | [268.29; 272.02] |
|
|
| Inp | 268.29 | NIST | |
| Inp | 272.02 | NIST | |
| S°gas | 778.31 | J/mol×K | NIST |
| S°liquid | [586.18; 626.80] | J/mol×K |
|
| S°liquid | 586.18 | J/mol×K | NIST |
| S°liquid | 626.80 | J/mol×K | NIST |
| Tboil | [543.00; 561.00] | K |
|
| Tboil | 560.01 | K | KDB |
| Tboil | 560.20 | K | NIST |
| Tboil | 559.00 ± 2.00 | K | NIST |
| Tboil | 559.92 ± 0.20 | K | NIST |
| Tboil | 553.00 ± 5.00 | K | NIST |
| Tboil | 556.00 ± 6.00 | K | NIST |
| Tboil | 561.00 ± 4.00 | K | NIST |
| Tboil | 548.00 ± 5.00 | K | NIST |
| Tboil | 543.00 ± 8.00 | K | NIST |
| Tboil | 547.00 ± 5.00 | K | NIST |
| Tboil | 551.00 ± 5.00 | K | NIST |
| Tc | 723.00 | K | KDB |
| Tfus | [288.00; 293.00] | K |
|
| Tfus | 291.34 | K | KDB |
| Tfus | 291.17 | K | Aq. Sol... |
| Tfus | 291.45 | K | Phase d... |
| Tfus | 291.50 | K | Experim... |
| Tfus | 291.10 | K | Phase e... |
| Tfus | 291.00 | K | Determi... |
| Tfus | 291.30 | K | Solid L... |
| Tfus | 291.27 ± 0.02 | K | NIST |
| Tfus | 291.32 ± 0.20 | K | NIST |
| Tfus | 291.19 ± 0.05 | K | NIST |
| Tfus | 291.15 ± 0.50 | K | NIST |
| Tfus | 291.00 ± 0.30 | K | NIST |
| Tfus | 291.33 ± 0.10 | K | NIST |
| Tfus | 291.25 ± 0.10 | K | NIST |
| Tfus | 290.00 ± 1.66 | K | NIST |
| Tfus | 291.00 ± 2.00 | K | NIST |
| Tfus | 291.29 ± 0.02 | K | NIST |
| Tfus | 291.29 ± 0.02 | K | NIST |
| Tfus | 291.30 ± 0.01 | K | NIST |
| Tfus | 291.30 ± 0.06 | K | NIST |
| Tfus | 291.30 ± 0.04 | K | NIST |
| Tfus | 291.31 ± 0.02 | K | NIST |
| Tfus | 291.00 ± 2.00 | K | NIST |
| Tfus | 290.00 ± 3.00 | K | NIST |
| Tfus | 291.21 ± 0.15 | K | NIST |
| Tfus | 291.24 ± 0.10 | K | NIST |
| Tfus | 291.24 ± 0.20 | K | NIST |
| Tfus | 290.80 ± 0.50 | K | NIST |
| Tfus | 291.29 ± 0.02 | K | NIST |
| Tfus | 291.29 ± 0.01 | K | NIST |
| Tfus | 291.24 ± 0.10 | K | NIST |
| Tfus | Outlier 293.00 ± 0.60 | K | NIST |
| Tfus | 291.30 ± 0.02 | K | NIST |
| Tfus | 291.20 ± 0.60 | K | NIST |
| Tfus | 290.40 ± 1.50 | K | NIST |
| Tfus | 291.20 ± 0.40 | K | NIST |
| Tfus | 291.00 ± 2.00 | K | NIST |
| Tfus | 291.33 ± 0.20 | K | NIST |
| Tfus | 291.30 ± 0.30 | K | NIST |
| Tfus | 290.60 ± 0.50 | K | NIST |
| Tfus | 291.29 ± 0.10 | K | NIST |
| Tfus | Outlier 293.00 ± 3.00 | K | NIST |
| Tfus | 292.40 ± 0.50 | K | NIST |
| Tfus | 290.20 ± 2.00 | K | NIST |
| Tfus | 291.00 ± 0.60 | K | NIST |
| Tfus | Outlier 288.00 ± 3.00 | K | NIST |
| Tfus | 291.05 ± 0.40 | K | NIST |
| Tfus | 290.10 ± 0.50 | K | NIST |
| Tfus | 290.98 ± 0.30 | K | NIST |
| Tfus | Outlier 288.69 ± 2.00 | K | NIST |
| Tfus | 290.70 ± 2.00 | K | NIST |
| Tfus | 291.26 ± 0.20 | K | NIST |
| Tfus | 290.00 ± 2.00 | K | NIST |
| Tfus | 291.26 ± 0.20 | K | NIST |
| Tfus | 291.00 ± 2.00 | K | NIST |
| Tfus | Outlier 293.00 ± 2.00 | K | NIST |
| Tfus | Outlier 293.00 ± 2.00 | K | NIST |
| Tfus | 291.40 ± 2.00 | K | NIST |
| Tfus | 292.00 ± 3.00 | K | NIST |
| Tfus | 291.00 ± 3.00 | K | NIST |
| Tfus | 291.00 ± 2.00 | K | NIST |
| Vc | [1.034; 1.034] | m3/kmol |
|
| Vc | 1.034 | m3/kmol | KDB |
| Vc | 1.034 | m3/kmol | NIST |
| Zc | 0.2408100 | KDB | |
| Zra | 0.24 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [611.73; 715.97] | J/mol×K | [565.48; 724.21] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 620 640 660 680 700 720 600 650 700 | ||||
| Cp,gas | 611.73 | J/mol×K | 565.48 | Joback Calculated Property |
| Cp,gas | 630.89 | J/mol×K | 591.94 | Joback Calculated Property |
| Cp,gas | 649.30 | J/mol×K | 618.39 | Joback Calculated Property |
| Cp,gas | 667.00 | J/mol×K | 644.85 | Joback Calculated Property |
| Cp,gas | 684.00 | J/mol×K | 671.30 | Joback Calculated Property |
| Cp,gas | 700.31 | J/mol×K | 697.76 | Joback Calculated Property |
| Cp,gas | 715.97 | J/mol×K | 724.21 | Joback Calculated Property |
| Cp,liquid | [484.90; 512.37] | J/mol×K | [297.79; 313.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 485 490 495 500 505 510 515 300 305 310 | ||||
| Cp,liquid | 499.00 | J/mol×K | 297.79 | NIST |
| Cp,liquid | 498.30 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 504.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 499.62 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 500.21 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 500.21 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 499.62 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 495.73 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 496.45 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 497.16 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 499.97 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 501.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 499.72 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 504.58 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 501.45 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 484.90 | J/mol×K | 311.00 | NIST |
| Cp,liquid | 512.37 | J/mol×K | 313.15 | NIST |
| η | [0.0001705; 0.0034910] | Pa×s | [293.15; 573.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 300 400 500 | ||||
| η | 0.0034910 | Pa×s | 293.15 | Viscome... |
| η | 0.0034860 | Pa×s | 293.15 | Liquid ... |
| η | 0.0030940 | Pa×s | 298.15 | Viscome... |
| η | 0.0030410 | Pa×s | 298.15 | Studies... |
| η | 0.0030410 | Pa×s | 298.15 | Volumet... |
| η | 0.0030410 | Pa×s | 298.15 | Tempera... |
| η | 0.0027060 | Pa×s | 303.15 | Tempera... |
| η | 0.0027060 | Pa×s | 303.15 | Volumet... |
| η | 0.0027780 | Pa×s | 303.15 | Viscome... |
| η | 0.0027720 | Pa×s | 303.15 | Liquid ... |
| η | 0.0027060 | Pa×s | 303.15 | Studies... |
| η | 0.0024090 | Pa×s | 308.15 | Volumet... |
| η | 0.0024090 | Pa×s | 308.15 | Studies... |
| η | 0.0024090 | Pa×s | 308.15 | Tempera... |
| η | 0.0022610 | Pa×s | 313.15 | Liquid ... |
| η | 0.0018400 | Pa×s | 323.15 | Liquid ... |
| η | 0.0012360 | Pa×s | 348.15 | Liquid ... |
| η | 0.0008927 | Pa×s | 373.15 | Liquid ... |
| η | 0.0006788 | Pa×s | 398.15 | Liquid ... |
| η | 0.0005351 | Pa×s | 423.15 | Liquid ... |
| η | 0.0004256 | Pa×s | 448.15 | Liquid ... |
| η | 0.0003440 | Pa×s | 473.15 | Liquid ... |
| η | 0.0002862 | Pa×s | 498.15 | Liquid ... |
| η | 0.0002360 | Pa×s | 523.15 | Liquid ... |
| η | 0.0001937 | Pa×s | 548.15 | Liquid ... |
| η | 0.0001705 | Pa×s | 573.15 | Liquid ... |
| ΔfusH | [47.55; 53.36] | kJ/mol | [290.70; 292.10] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 47 48 49 50 51 52 53 291 291.5 292 | ||||
| ΔfusH | 53.00 | kJ/mol | 290.70 | NIST |
| ΔfusH | 51.46 | kJ/mol | 291.10 | NIST |
| ΔfusH | 51.46 | kJ/mol | 291.10 | NIST |
| ΔfusH | 51.54 | kJ/mol | 291.10 | NIST |
| ΔfusH | 53.35 | kJ/mol | 291.30 | NIST |
| ΔfusH | 53.36 | kJ/mol | 291.34 | NIST |
| ΔfusH | 47.55 | kJ/mol | 292.10 | NIST |
| ΔsubH | [80.00; 134.90] | kJ/mol | [288.00; 291.00] |
|
| ΔsubH | 80.00 ± 3.00 | kJ/mol | 288.00 | NIST |
| ΔsubH | 83.00 ± 8.00 | kJ/mol | 289.00 | NIST |
| ΔsubH | 134.90 | kJ/mol | 291.00 | NIST |
| ΔvapH | [51.21; 93.40] | kJ/mol | [300.50; 560.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 50 60 70 80 90 300 400 500 | ||||
| ΔvapH | 80.20 | kJ/mol | 300.50 | NIST |
| ΔvapH | 93.40 | kJ/mol | 311.50 | NIST |
| ΔvapH | 66.90 | kJ/mol | 343.00 | NIST |
| ΔvapH | 72.90 | kJ/mol | 349.80 | Synthes... |
| ΔvapH | 74.50 | kJ/mol | 353.00 | Express... |
| ΔvapH | 66.20 | kJ/mol | 353.00 | NIST |
| ΔvapH | 65.60 | kJ/mol | 363.00 | NIST |
| ΔvapH | 64.90 | kJ/mol | 373.00 | NIST |
| ΔvapH | 74.90 | kJ/mol | 373.00 | NIST |
| ΔvapH | 64.20 | kJ/mol | 383.00 | NIST |
| ΔvapH | 65.70 | kJ/mol | 455.50 | NIST |
| ΔvapH | 68.50 | kJ/mol | 488.00 | NIST |
| ΔvapH | 61.70 | kJ/mol | 515.00 | NIST |
| ΔvapH | 59.80 | kJ/mol | 547.00 | NIST |
| ΔvapH | 51.21 | kJ/mol | 560.50 | KDB |
| Pvap | [6.01e-05; 102.04] | kPa | [284.15; 560.90] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 400 500 | ||||
| Pvap | 6.01e-05 | kPa | 284.15 | Determi... |
| Pvap | 1.02e-04 | kPa | 289.15 | Determi... |
| Pvap | 1.68e-04 | kPa | 294.15 | Determi... |
| Pvap | 2.74e-04 | kPa | 299.15 | Determi... |
| Pvap | 4.40e-04 | kPa | 304.15 | Determi... |
| Pvap | 6.96e-04 | kPa | 309.15 | Determi... |
| Pvap | 1.08e-03 | kPa | 314.15 | Determi... |
| Pvap | 1.66e-03 | kPa | 319.15 | Determi... |
| Pvap | 2.52e-03 | kPa | 324.15 | Determi... |
| Pvap | 3.77e-03 | kPa | 329.15 | Determi... |
| Pvap | 5.58e-03 | kPa | 334.15 | Determi... |
| Pvap | 8.16e-03 | kPa | 339.15 | Determi... |
| Pvap | 0.01 | kPa | 344.15 | Determi... |
| Pvap | 0.02 | kPa | 349.15 | Determi... |
| Pvap | 0.02 | kPa | 354.15 | Determi... |
| Pvap | 0.03 | kPa | 359.15 | Determi... |
| Pvap | 0.05 | kPa | 364.15 | Determi... |
| Pvap | 0.06 | kPa | 369.15 | Determi... |
| Pvap | 0.09 | kPa | 374.15 | Determi... |
| Pvap | 0.12 | kPa | 379.15 | Determi... |
| Pvap | 0.16 | kPa | 384.15 | Determi... |
| Pvap | 0.21 | kPa | 389.15 | Determi... |
| Pvap | 0.28 | kPa | 394.15 | Determi... |
| Pvap | 0.37 | kPa | 399.15 | Determi... |
| Pvap | 0.48 | kPa | 404.15 | Determi... |
| Pvap | 0.63 | kPa | 409.15 | Determi... |
| Pvap | 0.81 | kPa | 414.15 | Determi... |
| Pvap | 1.03 | kPa | 419.15 | Determi... |
| Pvap | 1.32 | kPa | 424.15 | Determi... |
| Pvap | 1.67 | kPa | 429.15 | Determi... |
| Pvap | 2.10 | kPa | 434.15 | Determi... |
| Pvap | 2.63 | kPa | 439.15 | Determi... |
| Pvap | 3.28 | kPa | 444.15 | Determi... |
| Pvap | 4.07 | kPa | 449.15 | Determi... |
| Pvap | 5.02 | kPa | 454.15 | Determi... |
| Pvap | 6.18 | kPa | 459.15 | Determi... |
| Pvap | 7.56 | kPa | 464.15 | Determi... |
| Pvap | 9.21 | kPa | 469.15 | Determi... |
| Pvap | 11.20 | kPa | 474.15 | Determi... |
| Pvap | 13.50 | kPa | 479.15 | Determi... |
| Pvap | 16.30 | kPa | 484.15 | Determi... |
| Pvap | 14.78 | kPa | 486.10 | Vapor p... |
| Pvap | 19.50 | kPa | 489.15 | Determi... |
| Pvap | 23.30 | kPa | 494.15 | Determi... |
| Pvap | 27.70 | kPa | 499.15 | Determi... |
| Pvap | 32.90 | kPa | 504.15 | Determi... |
| Pvap | 38.90 | kPa | 509.15 | Determi... |
| Pvap | 49.76 | kPa | 529.60 | Vapor p... |
| Pvap | 79.60 | kPa | 549.30 | Vapor p... |
| Pvap | 101.35 | kPa | 560.50 | Vapor p... |
| Pvap | 102.04 | kPa | 560.90 | Vapor p... |
| n0 | [1.41450; 1.43520] | [293.10; 343.15] |
|
|
|
T(K) Refractive Index 1.41 1.42 1.42 1.43 1.43 300 320 340 | ||||
| n0 | 1.43440 | 293.10 | Liquid-... | |
| n0 | 1.43520 | 293.15 | Densiti... | |
| n0 | 1.43460 | 293.15 | Experim... | |
| n0 | 1.43232 | 298.15 | Phase b... | |
| n0 | 1.43230 | 298.15 | Measure... | |
| n0 | 1.43250 | 298.15 | Liquid-... | |
| n0 | 1.43250 | 298.15 | Liquid-... | |
| n0 | 1.43400 | 298.15 | Densiti... | |
| n0 | 1.43232 | 298.15 | Thiophe... | |
| n0 | 1.43180 | 298.20 | Liquid-... | |
| n0 | 1.43110 | 303.15 | Densiti... | |
| n0 | 1.42690 | 313.15 | Densiti... | |
| n0 | 1.42280 | 323.15 | Densiti... | |
| n0 | 1.41870 | 333.15 | Densiti... | |
| n0 | 1.41450 | 343.15 | Densiti... | |
| ρl | [717.50; 773.70] | kg/m3 | [293.00; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 720 730 740 750 760 770 300 320 340 360 | ||||
| ρl | 773.00 | kg/m3 | 293.00 | KDB |
| ρl | 773.50 | kg/m3 | 293.15 | Liquid-... |
| ρl | 773.33 | kg/m3 | 293.15 | Densiti... |
| ρl | 773.37 | kg/m3 | 293.15 | Densiti... |
| ρl | 773.70 | kg/m3 | 293.15 | Density... |
| ρl | 773.49 | kg/m3 | 293.15 | Density... |
| ρl | 773.42 | kg/m3 | 293.15 | Density... |
| ρl | 769.91 | kg/m3 | 298.15 | Thermod... |
| ρl | 769.87 | kg/m3 | 298.15 | A syste... |
| ρl | 770.22 | kg/m3 | 298.15 | Thermod... |
| ρl | 771.50 | kg/m3 | 298.15 | Ternary... |
| ρl | 771.15 | kg/m3 | 298.15 | Solvent... |
| ρl | 770.31 | kg/m3 | 298.15 | Excess ... |
| ρl | 770.22 | kg/m3 | 298.15 | Liquid ... |
| ρl | 770.31 | kg/m3 | 298.15 | Excess ... |
| ρl | 770.31 | kg/m3 | 298.15 | Excess ... |
| ρl | 773.19 | kg/m3 | 298.15 | Binary ... |
| ρl | 769.92 | kg/m3 | 298.15 | Measure... |
| ρl | 770.22 | kg/m3 | 298.15 | Liquid ... |
| ρl | 770.30 | kg/m3 | 298.15 | Liquid ... |
| ρl | 770.21 | kg/m3 | 298.15 | Liquid-... |
| ρl | 770.14 | kg/m3 | 298.15 | Liquid-... |
| ρl | 773.19 | kg/m3 | 298.15 | (Liquid... |
| ρl | 769.86 | kg/m3 | 298.15 | Densiti... |
| ρl | 770.32 | kg/m3 | 298.15 | Thermod... |
| ρl | 769.93 | kg/m3 | 298.15 | Liquid-... |
| ρl | 769.81 | kg/m3 | 298.15 | Densiti... |
| ρl | 770.01 | kg/m3 | 298.15 | Liquid-... |
| ρl | 769.89 | kg/m3 | 298.15 | Densiti... |
| ρl | 770.30 | kg/m3 | 298.20 | Ternary... |
| ρl | 766.47 | kg/m3 | 303.15 | Density... |
| ρl | 766.55 | kg/m3 | 303.15 | Density... |
| ρl | 766.40 | kg/m3 | 303.15 | Densiti... |
| ρl | 766.80 | kg/m3 | 303.15 | Density... |
| ρl | 766.40 | kg/m3 | 303.15 | A syste... |
| ρl | 766.51 | kg/m3 | 303.15 | Measure... |
| ρl | 766.43 | kg/m3 | 303.15 | Densiti... |
| ρl | 762.95 | kg/m3 | 308.15 | A syste... |
| ρl | 762.94 | kg/m3 | 308.15 | Densiti... |
| ρl | 763.06 | kg/m3 | 308.15 | Measure... |
| ρl | 762.89 | kg/m3 | 308.15 | Densiti... |
| ρl | 759.60 | kg/m3 | 313.15 | Measure... |
| ρl | 759.63 | kg/m3 | 313.15 | Density... |
| ρl | 759.55 | kg/m3 | 313.15 | Experim... |
| ρl | 759.51 | kg/m3 | 313.15 | Densiti... |
| ρl | 759.48 | kg/m3 | 313.15 | Densiti... |
| ρl | 759.55 | kg/m3 | 313.15 | Density... |
| ρl | 762.90 | kg/m3 | 313.15 | Excess ... |
| ρl | 759.90 | kg/m3 | 313.15 | Density... |
| ρl | 755.98 | kg/m3 | 318.15 | Densiti... |
| ρl | 755.99 | kg/m3 | 318.15 | Densiti... |
| ρl | 756.14 | kg/m3 | 318.15 | Measure... |
| ρl | 752.63 | kg/m3 | 323.15 | Density... |
| ρl | 752.90 | kg/m3 | 323.15 | Density... |
| ρl | 752.58 | kg/m3 | 323.15 | Densiti... |
| ρl | 752.64 | kg/m3 | 323.15 | Experim... |
| ρl | 752.68 | kg/m3 | 323.15 | Measure... |
| ρl | 752.71 | kg/m3 | 323.15 | Density... |
| ρl | 752.60 | kg/m3 | 323.15 | Densiti... |
| ρl | 746.00 | kg/m3 | 333.15 | Density... |
| ρl | 745.71 | kg/m3 | 333.15 | Density... |
| ρl | 745.69 | kg/m3 | 333.15 | Densiti... |
| ρl | 745.79 | kg/m3 | 333.15 | Density... |
| ρl | 745.73 | kg/m3 | 333.15 | Experim... |
| ρl | 739.00 | kg/m3 | 343.15 | Density... |
| ρl | 738.80 | kg/m3 | 343.15 | Density... |
| ρl | 738.90 | kg/m3 | 343.15 | Density... |
| ρl | 731.80 | kg/m3 | 353.15 | Density... |
| ρl | 731.90 | kg/m3 | 353.15 | Density... |
| ρl | 724.70 | kg/m3 | 363.15 | Density... |
| ρl | 724.80 | kg/m3 | 363.15 | Density... |
| ρl | 717.70 | kg/m3 | 373.15 | Density... |
| ρl | 717.50 | kg/m3 | 373.15 | Density... |
| ΔfusS | [176.79; 183.15] | J/mol×K | [291.10; 291.34] |
|
| ΔfusS | 177.10 | J/mol×K | 291.10 | NIST |
| ΔfusS | 176.79 | J/mol×K | 291.10 | NIST |
| ΔfusS | 183.13 | J/mol×K | 291.30 | NIST |
| ΔfusS | 183.15 | J/mol×K | 291.34 | NIST |
| csound,fluid | [1074.00; 1367.20] | m/s | [290.65; 373.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1050 1100 1150 1200 1250 1300 1350 300 320 340 360 | ||||
| csound,fluid | 1367.20 | m/s | 290.65 | Density... |
| csound,fluid | 1365.30 | m/s | 291.15 | Density... |
| csound,fluid | 1363.40 | m/s | 291.65 | Density... |
| csound,fluid | 1361.50 | m/s | 292.15 | Density... |
| csound,fluid | 1359.60 | m/s | 292.65 | Density... |
| csound,fluid | 1356.00 | m/s | 293.00 | Fixed-P... |
| csound,fluid | 1357.70 | m/s | 293.15 | Density... |
| csound,fluid | 1357.40 | m/s | 293.15 | Densiti... |
| csound,fluid | 1357.00 | m/s | 293.15 | Tempera... |
| csound,fluid | 1340.00 | m/s | 298.00 | Fixed-P... |
| csound,fluid | 1338.00 | m/s | 298.15 | Tempera... |
| csound,fluid | 1338.80 | m/s | 298.15 | Density... |
| csound,fluid | 1325.00 | m/s | 303.00 | Fixed-P... |
| csound,fluid | 1320.20 | m/s | 303.15 | Density... |
| csound,fluid | 1319.60 | m/s | 303.15 | Densiti... |
| csound,fluid | 1312.00 | m/s | 303.15 | Tempera... |
| csound,fluid | 1301.70 | m/s | 308.15 | Density... |
| csound,fluid | 1301.00 | m/s | 308.15 | Tempera... |
| csound,fluid | 1287.00 | m/s | 313.00 | Fixed-P... |
| csound,fluid | 1283.40 | m/s | 313.15 | Density... |
| csound,fluid | 1283.00 | m/s | 313.15 | Tempera... |
| csound,fluid | 1282.90 | m/s | 313.15 | Densiti... |
| csound,fluid | 1268.00 | m/s | 318.00 | Fixed-P... |
| csound,fluid | 1265.00 | m/s | 318.15 | Tempera... |
| csound,fluid | 1265.30 | m/s | 318.15 | Density... |
| csound,fluid | 1248.00 | m/s | 323.00 | Fixed-P... |
| csound,fluid | 1246.00 | m/s | 323.15 | Tempera... |
| csound,fluid | 1247.40 | m/s | 323.15 | Density... |
| csound,fluid | 1247.00 | m/s | 323.15 | Densiti... |
| csound,fluid | 1227.00 | m/s | 328.00 | Fixed-P... |
| csound,fluid | 1228.00 | m/s | 328.15 | Tempera... |
| csound,fluid | 1229.80 | m/s | 328.15 | Density... |
| csound,fluid | 1210.00 | m/s | 333.00 | Fixed-P... |
| csound,fluid | 1212.30 | m/s | 333.15 | Density... |
| csound,fluid | 1211.00 | m/s | 333.15 | Tempera... |
| csound,fluid | 1212.10 | m/s | 333.15 | Densiti... |
| csound,fluid | 1194.90 | m/s | 338.15 | Density... |
| csound,fluid | 1193.00 | m/s | 338.15 | Tempera... |
| csound,fluid | 1176.00 | m/s | 343.15 | Tempera... |
| csound,fluid | 1177.90 | m/s | 343.15 | Density... |
| csound,fluid | 1158.00 | m/s | 348.15 | Tempera... |
| csound,fluid | 1141.00 | m/s | 353.15 | Tempera... |
| csound,fluid | 1124.00 | m/s | 358.15 | Tempera... |
| csound,fluid | 1107.00 | m/s | 363.15 | Tempera... |
| csound,fluid | 1090.00 | m/s | 368.15 | Tempera... |
| csound,fluid | 1074.00 | m/s | 373.15 | Tempera... |
| γ | [0.03; 0.03] | N/m | [294.00; 313.20] |
|
| γ | 0.03 | N/m | 294.00 | Densiti... |
| γ | 0.03 | N/m | 294.80 | Density... |
| γ | 0.03 | N/m | 313.20 | KDB |
| vspec | [0.00; 0.00] | m3/kg | [298.00; 573.00] |
|
|
T(K) Specific Volume (m3/kg) 1.30e-3 1.40e-3 1.50e-3 1.60e-3 1.70e-3 1.80e-3 300 400 500 | ||||
| vspec | 0.00 | m3/kg | 298.00 | A simpl... |
| vspec | 0.00 | m3/kg | 323.00 | A simpl... |
| vspec | 0.00 | m3/kg | 348.00 | A simpl... |
| vspec | 0.00 | m3/kg | 373.00 | A simpl... |
| vspec | 0.00 | m3/kg | 398.00 | A simpl... |
| vspec | 0.00 | m3/kg | 423.00 | A simpl... |
| vspec | 0.00 | m3/kg | 448.00 | A simpl... |
| vspec | 0.00 | m3/kg | 473.00 | A simpl... |
| vspec | 0.00 | m3/kg | 498.00 | A simpl... |
| vspec | 0.00 | m3/kg | 523.00 | A simpl... |
| vspec | 0.00 | m3/kg | 548.00 | A simpl... |
| vspec | 0.00 | m3/kg | 573.00 | A simpl... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [444.06; 496.42] | K | [3.47; 22.39] |
|
|
P(kPa) Boiling point at given pressure (K) 440 450 460 470 480 490 500 5 10 15 20 | ||||
| Tboil | 444.06 | K | 3.47 | Improvi... |
| Tboil | 474.05 | K | 10.37 | Improvi... |
| Tboil | 486.81 | K | 15.17 | Improvi... |
| Tboil | 493.60 | K | 18.66 | Improvi... |
| Tboil | 496.42 | K | 22.39 | Improvi... |
| Tfus | [291.50; 343.15] | K | [100.00; 251030.00] |
|
|
P(kPa) Melting point (K) 290 300 310 320 330 340 0 100000 200000 | ||||
| Tfus | 291.50 | K | 100.00 | Liquid ... |
| Tfus | 293.15 | K | 9210.00 | Influen... |
| Tfus | 293.15 | K | 9210.00 | High pr... |
| Tfus | 296.00 | K | 20000.00 | Liquid ... |
| Tfus | 300.40 | K | 40000.00 | Liquid ... |
| Tfus | 303.15 | K | 50650.00 | High pr... |
| Tfus | 303.15 | K | 50650.00 | Influen... |
| Tfus | 304.80 | K | 60000.00 | Liquid ... |
| Tfus | 309.70 | K | 80000.00 | Liquid ... |
| Tfus | 313.15 | K | 95560.00 | Influen... |
| Tfus | 313.15 | K | 95560.00 | High pr... |
| Tfus | 313.50 | K | 100000.00 | Liquid ... |
| Tfus | 323.15 | K | 143920.00 | Influen... |
| Tfus | 323.15 | K | 143920.00 | High pr... |
| Tfus | 333.15 | K | 195740.00 | High pr... |
| Tfus | 333.15 | K | 195740.00 | Influen... |
| Tfus | 343.15 | K | 251030.00 | High pr... |
| Tfus | 343.15 | K | 251030.00 | Influen... |
Datasets
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 323.15 | 130.00 | 513.57 |
| 328.15 | 130.00 | 517.19 |
| 333.15 | 130.00 | 520.81 |
| 338.15 | 130.00 | 524.66 |
| 343.15 | 130.00 | 528.51 |
| 348.15 | 130.00 | 532.82 |
| 353.15 | 130.00 | 536.44 |
| 358.15 | 130.00 | 540.74 |
| 363.15 | 130.00 | 544.59 |
| 368.15 | 130.00 | 548.67 |
| 373.15 | 130.00 | 553.20 |
| 378.15 | 130.00 | 557.27 |
| 383.15 | 130.00 | 561.57 |
| 388.15 | 130.00 | 565.65 |
| 393.15 | 130.00 | 569.73 |
| 398.15 | 130.00 | 574.03 |
| 403.15 | 130.00 | 578.56 |
| 408.15 | 130.00 | 583.09 |
| 413.15 | 130.00 | 586.94 |
| 418.15 | 130.00 | 591.46 |
| 423.15 | 130.00 | 595.77 |
| 428.15 | 130.00 | 599.62 |
| 433.15 | 130.00 | 603.92 |
| 438.15 | 130.00 | 608.67 |
| 443.15 | 130.00 | 613.20 |
| 448.15 | 130.00 | 617.28 |
| 453.15 | 130.00 | 622.26 |
| 323.15 | 10090.00 | 512.21 |
| 328.15 | 10090.00 | 515.83 |
| 333.15 | 10090.00 | 519.46 |
| 338.15 | 10090.00 | 523.31 |
| 343.15 | 10090.00 | 526.48 |
| 348.15 | 10090.00 | 530.10 |
| 353.15 | 10090.00 | 534.40 |
| 358.15 | 10090.00 | 538.48 |
| 363.15 | 10090.00 | 542.10 |
| 368.15 | 10090.00 | 546.40 |
| 373.15 | 10090.00 | 550.70 |
| 378.15 | 10090.00 | 554.55 |
| 383.15 | 10090.00 | 558.86 |
| 388.15 | 10090.00 | 563.16 |
| 393.15 | 10090.00 | 567.24 |
| 398.15 | 10090.00 | 571.31 |
| 403.15 | 10090.00 | 575.61 |
| 408.15 | 10090.00 | 579.92 |
| 413.15 | 10090.00 | 584.44 |
| 418.15 | 10090.00 | 588.97 |
| 423.15 | 10090.00 | 593.05 |
| 428.15 | 10090.00 | 596.45 |
| 433.15 | 10090.00 | 600.30 |
| 438.15 | 10090.00 | 604.60 |
| 443.15 | 10090.00 | 609.35 |
| 448.15 | 10090.00 | 613.66 |
| 453.15 | 10090.00 | 617.05 |
| 458.15 | 10090.00 | 621.35 |
| 463.15 | 10090.00 | 625.43 |
| 468.15 | 10090.00 | 630.19 |
| 473.15 | 10090.00 | 634.94 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.90 | 3300.00 | 0.0028 |
| 303.90 | 7300.00 | 0.0030 |
| 303.90 | 12900.00 | 0.0032 |
| 303.90 | 19000.00 | 0.0035 |
| 303.90 | 26800.00 | 0.0038 |
| 303.90 | 33600.00 | 0.0041 |
| 325.70 | 8100.00 | 0.0019 |
| 325.70 | 8300.00 | 0.0020 |
| 325.70 | 21500.00 | 0.0023 |
| 325.70 | 35600.00 | 0.0027 |
| 325.70 | 49300.00 | 0.0031 |
| 325.70 | 63600.00 | 0.0036 |
| 325.70 | 77500.00 | 0.0041 |
| 325.70 | 91800.00 | 0.0046 |
| 325.70 | 104100.00 | 0.0052 |
| 325.70 | 119200.00 | 0.0059 |
| 325.70 | 122700.00 | 0.0061 |
| 429.10 | 12800.00 | 0.0006 |
| 429.10 | 12800.00 | 0.0006 |
| 429.10 | 22200.00 | 0.0006 |
| 429.10 | 22700.00 | 0.0006 |
| 429.10 | 35800.00 | 0.0007 |
| 429.10 | 70500.00 | 0.0010 |
| 429.10 | 91600.00 | 0.0012 |
| 429.10 | 118800.00 | 0.0014 |
| 429.10 | 140300.00 | 0.0016 |
| 429.10 | 167800.00 | 0.0018 |
| 429.10 | 188000.00 | 0.0020 |
| 429.10 | 222900.00 | 0.0025 |
| 533.70 | 14100.00 | 0.0003 |
| 533.70 | 14300.00 | 0.0003 |
| 533.70 | 29900.00 | 0.0003 |
| 533.70 | 30100.00 | 0.0003 |
| 533.70 | 50400.00 | 0.0004 |
| 533.70 | 50500.00 | 0.0004 |
| 533.70 | 77100.00 | 0.0005 |
| 533.70 | 104600.00 | 0.0006 |
| 533.70 | 125000.00 | 0.0007 |
| 533.70 | 152800.00 | 0.0008 |
| 533.70 | 188400.00 | 0.0010 |
| 533.70 | 210000.00 | 0.0011 |
| 533.70 | 226600.00 | 0.0012 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 323.70 | 970.00 | 0.0019 |
| 322.70 | 1940.00 | 0.0019 |
| 323.80 | 1980.00 | 0.0019 |
| 323.70 | 3000.00 | 0.0019 |
| 323.80 | 3910.00 | 0.0019 |
| 372.70 | 990.00 | 0.0009 |
| 372.70 | 1960.00 | 0.0009 |
| 372.80 | 2970.00 | 0.0009 |
| 372.80 | 3950.00 | 0.0009 |
| 373.90 | 980.00 | 0.0009 |
| 373.90 | 2000.00 | 0.0009 |
| 373.90 | 2980.00 | 0.0009 |
| 373.90 | 3900.00 | 0.0009 |
| 422.90 | 1990.00 | 0.0006 |
| 422.90 | 2970.00 | 0.0006 |
| 422.90 | 3840.00 | 0.0006 |
| 471.90 | 1000.00 | 0.0004 |
| 472.00 | 2010.00 | 0.0004 |
| 472.10 | 2910.00 | 0.0004 |
| 472.10 | 3870.00 | 0.0004 |
| 473.70 | 3990.00 | 0.0004 |
| 521.90 | 970.00 | 0.0002 |
| 521.90 | 1960.00 | 0.0003 |
| 521.90 | 2950.00 | 0.0003 |
| 522.00 | 3830.00 | 0.0003 |
| 572.20 | 2000.00 | 0.0002 |
| 572.10 | 2930.00 | 0.0002 |
| 572.20 | 3850.00 | 0.0002 |
| 621.90 | 2010.00 | 0.0001 |
| 622.00 | 2890.00 | 0.0001 |
| 622.10 | 3820.00 | 0.0001 |
| 623.20 | 3990.00 | 0.0001 |
| 673.20 | 2000.00 | 0.0001 |
| 673.60 | 3000.00 | 0.0001 |
| 672.60 | 3990.00 | 0.0001 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 318.15 | 6895.00 | 0.0022 |
| 318.15 | 13790.00 | 0.0023 |
| 318.15 | 20680.00 | 0.0025 |
| 318.15 | 27580.00 | 0.0027 |
| 318.15 | 34470.00 | 0.0029 |
| 318.15 | 41370.00 | 0.0032 |
| 318.15 | 48260.00 | 0.0034 |
| 318.15 | 55160.00 | 0.0036 |
| 318.15 | 62050.00 | 0.0039 |
| 333.15 | 6895.00 | 0.0017 |
| 333.15 | 13790.00 | 0.0018 |
| 333.15 | 20680.00 | 0.0020 |
| 333.15 | 27580.00 | 0.0021 |
| 333.15 | 34470.00 | 0.0022 |
| 333.15 | 41370.00 | 0.0024 |
| 333.15 | 48260.00 | 0.0026 |
| 333.15 | 55160.00 | 0.0028 |
| 333.15 | 62050.00 | 0.0030 |
| 348.15 | 6895.00 | 0.0013 |
| 348.15 | 13790.00 | 0.0014 |
| 348.15 | 20680.00 | 0.0016 |
| 348.15 | 27580.00 | 0.0017 |
| 348.15 | 34470.00 | 0.0018 |
| 348.15 | 41370.00 | 0.0019 |
| 348.15 | 48260.00 | 0.0021 |
| 348.15 | 55160.00 | 0.0022 |
| 348.15 | 62050.00 | 0.0024 |
| 363.15 | 6895.00 | 0.0011 |
| 363.15 | 13790.00 | 0.0012 |
| 363.15 | 20680.00 | 0.0013 |
| 363.15 | 27580.00 | 0.0014 |
| 363.15 | 34470.00 | 0.0015 |
| 363.15 | 41370.00 | 0.0016 |
| 363.15 | 48260.00 | 0.0017 |
| 363.15 | 55160.00 | 0.0018 |
| 363.15 | 62050.00 | 0.0019 |
| 388.15 | 6895.00 | 0.0008 |
| 388.15 | 13790.00 | 0.0009 |
| 388.15 | 20680.00 | 0.0010 |
| 388.15 | 27580.00 | 0.0010 |
| 388.15 | 34470.00 | 0.0012 |
| 388.15 | 41370.00 | 0.0012 |
| 388.15 | 48260.00 | 0.0013 |
| 388.15 | 55160.00 | 0.0013 |
| 388.15 | 62050.00 | 0.0014 |
| 413.15 | 6895.00 | 0.0006 |
| 413.15 | 13790.00 | 0.0007 |
| 413.15 | 20680.00 | 0.0007 |
| 413.15 | 27580.00 | 0.0008 |
| 413.15 | 34470.00 | 0.0008 |
| 413.15 | 41370.00 | 0.0009 |
| 413.15 | 48260.00 | 0.0009 |
| 413.15 | 55160.00 | 0.0010 |
| 413.15 | 62050.00 | 0.0010 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 323.65 | 14900.00 | 758.0 |
| 323.65 | 27900.00 | 769.0 |
| 323.65 | 41500.00 | 779.0 |
| 323.65 | 55500.00 | 787.0 |
| 323.65 | 69400.00 | 792.0 |
| 323.65 | 81300.00 | 799.0 |
| 323.65 | 109700.00 | 807.0 |
| 422.85 | 14100.00 | 700.0 |
| 422.85 | 27900.00 | 713.0 |
| 422.85 | 41200.00 | 724.0 |
| 422.85 | 55500.00 | 734.0 |
| 422.85 | 69800.00 | 743.0 |
| 422.85 | 82800.00 | 750.0 |
| 422.85 | 108800.00 | 765.0 |
| 422.85 | 136900.00 | 778.0 |
| 422.85 | 170700.00 | 792.0 |
| 422.85 | 204300.00 | 804.0 |
| 422.85 | 236500.00 | 815.0 |
| 422.85 | 262300.00 | 823.0 |
| 522.55 | 15100.00 | 643.0 |
| 522.55 | 27100.00 | 660.0 |
| 522.55 | 42000.00 | 675.0 |
| 522.55 | 55400.00 | 687.0 |
| 522.55 | 69100.00 | 698.0 |
| 522.55 | 82100.00 | 707.0 |
| 522.55 | 107900.00 | 723.0 |
| 522.55 | 135800.00 | 738.0 |
| 522.55 | 170100.00 | 755.0 |
| 522.55 | 203300.00 | 769.0 |
| 522.55 | 235800.00 | 782.0 |
| 522.55 | 255000.00 | 788.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 769.98 |
| 313.15 | 100.00 | 759.6 |
| 333.15 | 100.00 | 745.81 |
| 373.15 | 100.00 | 717.79 |
| 393.15 | 100.00 | 703.59 |
| 433.15 | 100.00 | 674.64 |
| 298.15 | 10100.00 | 776.41 |
| 313.15 | 10100.00 | 766.44 |
| 373.15 | 10100.00 | 727.21 |
| 393.15 | 10100.00 | 714.02 |
| 433.15 | 10100.00 | 687.77 |
| 298.15 | 20100.00 | 782.34 |
| 313.15 | 20100.00 | 772.76 |
| 333.15 | 20100.00 | 760.5 |
| 373.15 | 20100.00 | 735.47 |
| 393.15 | 20100.00 | 723.09 |
| 433.15 | 20100.00 | 698.82 |
| 313.15 | 30100.00 | 778.65 |
| 373.15 | 30100.00 | 742.97 |
| 313.15 | 40100.00 | 784.24 |
| 333.15 | 40100.00 | 773.01 |
| 373.15 | 40100.00 | 749.88 |
| 393.15 | 40100.00 | 738.85 |
| 433.15 | 40100.00 | 717.04 |
| 333.15 | 50100.00 | 778.56 |
| 373.15 | 50100.00 | 756.25 |
| 313.15 | 60100.00 | 794.38 |
| 333.15 | 60100.00 | 783.47 |
| 373.15 | 60100.00 | 762.2 |
| 393.15 | 60100.00 | 752.0 |
| 433.15 | 60100.00 | 731.95 |
| 313.15 | 80100.00 | 803.42 |
| 333.15 | 80100.00 | 793.1 |
| 373.15 | 80100.00 | 773.03 |
| 393.15 | 80100.00 | 763.28 |
| 433.15 | 80100.00 | 744.68 |
| 333.15 | 100100.00 | 801.83 |
| 373.15 | 100100.00 | 782.74 |
| 393.15 | 100100.00 | 773.48 |
| 433.15 | 100100.00 | 755.89 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 770.5 |
| 298.15 | 1000.00 | 771.1 |
| 298.15 | 5000.00 | 773.6 |
| 298.15 | 10000.00 | 776.9 |
| 298.15 | 20000.00 | 782.6 |
| 298.15 | 30000.00 | 788.1 |
| 323.15 | 100.00 | 753.1 |
| 323.15 | 1000.00 | 753.9 |
| 323.15 | 5000.00 | 756.8 |
| 323.15 | 10000.00 | 760.4 |
| 323.15 | 20000.00 | 766.9 |
| 323.15 | 30000.00 | 772.9 |
| 323.15 | 40000.00 | 778.5 |
| 323.15 | 50000.00 | 783.8 |
| 323.15 | 60000.00 | 788.7 |
| 348.15 | 100.00 | 735.6 |
| 348.15 | 1000.00 | 736.5 |
| 348.15 | 5000.00 | 739.8 |
| 348.15 | 10000.00 | 743.8 |
| 348.15 | 20000.00 | 751.1 |
| 348.15 | 30000.00 | 757.8 |
| 348.15 | 40000.00 | 763.9 |
| 348.15 | 50000.00 | 769.7 |
| 348.15 | 60000.00 | 775.1 |
| 373.15 | 100.00 | 717.8 |
| 373.15 | 1000.00 | 719.4 |
| 373.15 | 5000.00 | 723.2 |
| 373.15 | 10000.00 | 727.7 |
| 373.15 | 20000.00 | 735.9 |
| 373.15 | 30000.00 | 743.4 |
| 373.15 | 40000.00 | 750.3 |
| 373.15 | 50000.00 | 756.5 |
| 373.15 | 60000.00 | 762.4 |
| 423.15 | 100.00 | 680.8 |
| 423.15 | 1000.00 | 684.1 |
| 423.15 | 5000.00 | 689.2 |
| 423.15 | 10000.00 | 695.1 |
| 423.15 | 20000.00 | 705.5 |
| 423.15 | 30000.00 | 714.7 |
| 423.15 | 40000.00 | 722.9 |
| 423.15 | 50000.00 | 730.4 |
| 423.15 | 60000.00 | 737.2 |
| 463.15 | 100.00 | 651.6 |
| 463.15 | 1000.00 | 654.5 |
| 463.15 | 5000.00 | 661.0 |
| 463.15 | 10000.00 | 668.5 |
| 463.15 | 20000.00 | 681.2 |
| 463.15 | 30000.00 | 692.0 |
| 463.15 | 40000.00 | 701.4 |
| 463.15 | 50000.00 | 709.8 |
| 463.15 | 60000.00 | 717.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.20 | 10000.00 | 775.86 |
| 303.20 | 10000.00 | 773.66 |
| 313.20 | 10000.00 | 764.59 |
| 323.20 | 10000.00 | 759.8 |
| 333.20 | 10000.00 | 753.38 |
| 348.20 | 10000.00 | 744.11 |
| 353.20 | 10000.00 | 740.03 |
| 373.20 | 10000.00 | 727.81 |
| 393.20 | 10000.00 | 713.25 |
| 413.20 | 10000.00 | 700.27 |
| 423.20 | 10000.00 | 694.3 |
| 433.20 | 10000.00 | 687.01 |
| 453.20 | 10000.00 | 674.02 |
| 463.20 | 10000.00 | 669.34 |
| 473.20 | 10000.00 | 660.45 |
| 298.20 | 20000.00 | 782.89 |
| 303.20 | 20000.00 | 779.38 |
| 313.20 | 20000.00 | 773.09 |
| 323.20 | 20000.00 | 766.48 |
| 333.20 | 20000.00 | 760.44 |
| 348.20 | 20000.00 | 751.32 |
| 353.20 | 20000.00 | 748.27 |
| 373.20 | 20000.00 | 736.02 |
| 393.20 | 20000.00 | 723.64 |
| 413.20 | 20000.00 | 711.23 |
| 423.20 | 20000.00 | 705.01 |
| 433.20 | 20000.00 | 698.74 |
| 453.20 | 20000.00 | 686.53 |
| 463.20 | 20000.00 | 680.32 |
| 473.20 | 20000.00 | 673.95 |
| 298.20 | 30000.00 | 788.75 |
| 303.20 | 30000.00 | 785.01 |
| 313.20 | 30000.00 | 778.81 |
| 323.20 | 30000.00 | 773.19 |
| 333.20 | 30000.00 | 767.3 |
| 348.20 | 30000.00 | 758.67 |
| 353.20 | 30000.00 | 755.72 |
| 373.20 | 30000.00 | 744.18 |
| 393.20 | 30000.00 | 732.3 |
| 413.20 | 30000.00 | 720.49 |
| 423.20 | 30000.00 | 714.62 |
| 433.20 | 30000.00 | 708.69 |
| 453.20 | 30000.00 | 696.77 |
| 463.20 | 30000.00 | 690.8 |
| 473.20 | 30000.00 | 685.23 |
| 298.20 | 40000.00 | 793.81 |
| 303.20 | 40000.00 | 790.38 |
| 313.20 | 40000.00 | 784.36 |
| 323.20 | 40000.00 | 778.83 |
| 333.20 | 40000.00 | 773.53 |
| 348.20 | 40000.00 | 765.1 |
| 353.20 | 40000.00 | 762.19 |
| 373.20 | 40000.00 | 751.02 |
| 393.20 | 40000.00 | 739.4 |
| 413.20 | 40000.00 | 728.42 |
| 423.20 | 40000.00 | 722.88 |
| 433.20 | 40000.00 | 717.4 |
| 453.20 | 40000.00 | 706.13 |
| 463.20 | 40000.00 | 700.49 |
| 473.20 | 40000.00 | 695.19 |
| 298.20 | 50000.00 | 799.18 |
| 303.20 | 50000.00 | 795.64 |
| 313.20 | 50000.00 | 789.46 |
| 323.20 | 50000.00 | 784.38 |
| 333.20 | 50000.00 | 779.1 |
| 348.20 | 50000.00 | 770.98 |
| 353.20 | 50000.00 | 768.11 |
| 373.20 | 50000.00 | 757.42 |
| 393.20 | 50000.00 | 746.41 |
| 413.20 | 50000.00 | 735.85 |
| 423.20 | 50000.00 | 730.73 |
| 433.20 | 50000.00 | 725.14 |
| 453.20 | 50000.00 | 714.59 |
| 463.20 | 50000.00 | 709.18 |
| 473.20 | 50000.00 | 704.05 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 318.15 | 6895.00 | 760.3 |
| 318.15 | 13789.00 | 765.0 |
| 318.15 | 20684.00 | 769.6 |
| 318.15 | 27579.00 | 773.9 |
| 318.15 | 34474.00 | 777.7 |
| 318.15 | 41369.00 | 781.5 |
| 318.15 | 48263.00 | 785.2 |
| 318.15 | 55158.00 | 788.7 |
| 318.15 | 62053.00 | 791.7 |
| 333.15 | 6895.00 | 750.7 |
| 333.15 | 13789.00 | 755.8 |
| 333.15 | 20684.00 | 760.4 |
| 333.15 | 27579.00 | 765.1 |
| 333.15 | 34474.00 | 769.7 |
| 333.15 | 41369.00 | 773.9 |
| 333.15 | 48263.00 | 777.6 |
| 333.15 | 55158.00 | 781.2 |
| 333.15 | 62053.00 | 784.3 |
| 348.15 | 6895.00 | 741.7 |
| 348.15 | 13789.00 | 747.2 |
| 348.15 | 20684.00 | 752.5 |
| 348.15 | 27579.00 | 757.2 |
| 348.15 | 34474.00 | 761.9 |
| 348.15 | 41369.00 | 766.1 |
| 348.15 | 48263.00 | 770.2 |
| 348.15 | 55158.00 | 774.1 |
| 348.15 | 62053.00 | 777.6 |
| 363.15 | 6895.00 | 732.0 |
| 363.15 | 13789.00 | 738.1 |
| 363.15 | 20684.00 | 743.9 |
| 363.15 | 27579.00 | 748.6 |
| 363.15 | 34474.00 | 753.7 |
| 363.15 | 41369.00 | 758.4 |
| 363.15 | 48263.00 | 762.6 |
| 363.15 | 55158.00 | 766.7 |
| 363.15 | 62053.00 | 770.5 |
| 388.15 | 6895.00 | 714.7 |
| 388.15 | 13789.00 | 721.7 |
| 388.15 | 20684.00 | 728.1 |
| 388.15 | 27579.00 | 733.9 |
| 388.15 | 34474.00 | 739.2 |
| 388.15 | 41369.00 | 744.1 |
| 388.15 | 48263.00 | 748.8 |
| 388.15 | 55158.00 | 753.3 |
| 388.15 | 62053.00 | 757.5 |
| 413.15 | 6895.00 | 696.2 |
| 413.15 | 13789.00 | 704.3 |
| 413.15 | 20684.00 | 711.0 |
| 413.15 | 27579.00 | 717.9 |
| 413.15 | 34474.00 | 723.7 |
| 413.15 | 41369.00 | 729.4 |
| 413.15 | 48263.00 | 734.5 |
| 413.15 | 55158.00 | 739.5 |
| 413.15 | 62053.00 | 743.8 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.15 | 340.00 | 759.52 |
| 313.15 | 690.00 | 759.83 |
| 313.15 | 1030.00 | 760.08 |
| 313.15 | 1380.00 | 760.33 |
| 313.15 | 1720.00 | 760.65 |
| 313.15 | 2070.00 | 760.88 |
| 313.15 | 2410.00 | 761.08 |
| 313.15 | 2760.00 | 761.33 |
| 313.15 | 3100.00 | 761.65 |
| 313.15 | 3450.00 | 761.83 |
| 313.15 | 3800.00 | 762.08 |
| 313.15 | 4140.00 | 762.33 |
| 313.15 | 4480.00 | 762.49 |
| 313.15 | 4830.00 | 762.83 |
| 313.15 | 5170.00 | 763.08 |
| 313.15 | 5510.00 | 763.33 |
| 313.15 | 5860.00 | 763.58 |
| 313.15 | 6200.00 | 763.83 |
| 313.15 | 6550.00 | 764.08 |
| 313.15 | 6890.00 | 764.33 |
| 313.15 | 7240.00 | 764.65 |
| 313.15 | 7580.00 | 764.83 |
| 313.15 | 7930.00 | 765.08 |
| 313.15 | 8270.00 | 765.33 |
| 313.15 | 8620.00 | 765.58 |
| 313.15 | 8960.00 | 765.74 |
| 313.15 | 9310.00 | 765.99 |
| 313.15 | 9650.00 | 766.24 |
| 313.15 | 10000.00 | 766.49 |
| 313.15 | 10340.00 | 766.74 |
| 313.15 | 10690.00 | 766.98 |
| 313.15 | 11030.00 | 767.22 |
| 313.15 | 11380.00 | 767.48 |
| 333.15 | 340.00 | 746.8 |
| 333.15 | 690.00 | 747.1 |
| 333.15 | 1030.00 | 747.4 |
| 333.15 | 1380.00 | 747.7 |
| 333.15 | 1720.00 | 748.0 |
| 333.15 | 2070.00 | 748.2 |
| 333.15 | 2410.00 | 748.5 |
| 333.15 | 2760.00 | 748.7 |
| 333.15 | 3100.00 | 749.0 |
| 333.15 | 3450.00 | 749.2 |
| 333.15 | 3800.00 | 749.5 |
| 333.15 | 4140.00 | 749.8 |
| 333.15 | 4480.00 | 750.0 |
| 333.15 | 4830.00 | 750.2 |
| 333.15 | 5170.00 | 750.5 |
| 333.15 | 5510.00 | 750.7 |
| 333.15 | 5860.00 | 751.0 |
| 333.15 | 6200.00 | 751.2 |
| 333.15 | 6550.00 | 751.4 |
| 333.15 | 6890.00 | 751.6 |
| 333.15 | 7240.00 | 752.0 |
| 333.15 | 7580.00 | 752.4 |
| 333.15 | 7930.00 | 752.6 |
| 333.15 | 8270.00 | 752.8 |
| 333.15 | 8620.00 | 753.0 |
| 333.15 | 8960.00 | 753.2 |
| 333.15 | 9310.00 | 753.5 |
| 333.15 | 9650.00 | 753.8 |
| 333.15 | 10000.00 | 754.0 |
| 333.15 | 10340.00 | 754.3 |
| 333.15 | 10690.00 | 754.5 |
| 333.15 | 11030.00 | 754.8 |
| 333.15 | 11380.00 | 755.0 |
| 353.15 | 340.00 | 736.2 |
| 353.15 | 690.00 | 736.4 |
| 353.15 | 1030.00 | 736.6 |
| 353.15 | 1380.00 | 736.9 |
| 353.15 | 1720.00 | 737.1 |
| 353.15 | 2070.00 | 737.4 |
| 353.15 | 2410.00 | 737.7 |
| 353.15 | 2760.00 | 738.0 |
| 353.15 | 3100.00 | 738.3 |
| 353.15 | 3450.00 | 738.7 |
| 353.15 | 3800.00 | 739.1 |
| 353.15 | 4140.00 | 739.3 |
| 353.15 | 4480.00 | 739.5 |
| 353.15 | 4830.00 | 739.8 |
| 353.15 | 5170.00 | 740.0 |
| 353.15 | 5510.00 | 740.2 |
| 353.15 | 5860.00 | 740.4 |
| 353.15 | 6200.00 | 740.5 |
| 353.15 | 6550.00 | 740.7 |
| 353.15 | 6890.00 | 741.0 |
| 353.15 | 7240.00 | 741.2 |
| 353.15 | 7580.00 | 741.5 |
| 353.15 | 7930.00 | 741.7 |
| 353.15 | 8270.00 | 742.0 |
| 353.15 | 8620.00 | 742.2 |
| 353.15 | 8960.00 | 742.5 |
| 353.15 | 9310.00 | 742.7 |
| 353.15 | 9650.00 | 742.9 |
| 353.15 | 10000.00 | 743.1 |
| 353.15 | 10340.00 | 743.5 |
| 353.15 | 10690.00 | 743.9 |
| 353.15 | 11030.00 | 744.1 |
| 353.15 | 11380.00 | 744.3 |
| 373.15 | 340.00 | 723.1 |
| 373.15 | 690.00 | 723.3 |
| 373.15 | 1030.00 | 723.6 |
| 373.15 | 1380.00 | 723.8 |
| 373.15 | 1720.00 | 724.0 |
| 373.15 | 2070.00 | 724.3 |
| 373.15 | 2410.00 | 724.6 |
| 373.15 | 2760.00 | 724.9 |
| 373.15 | 3100.00 | 725.1 |
| 373.15 | 3450.00 | 725.4 |
| 373.15 | 3800.00 | 725.6 |
| 373.15 | 4140.00 | 725.9 |
| 373.15 | 4480.00 | 726.1 |
| 373.15 | 4830.00 | 726.4 |
| 373.15 | 5170.00 | 726.7 |
| 373.15 | 5510.00 | 726.9 |
| 373.15 | 5860.00 | 727.2 |
| 373.15 | 6200.00 | 727.5 |
| 373.15 | 6550.00 | 727.8 |
| 373.15 | 6890.00 | 728.1 |
| 373.15 | 7240.00 | 728.4 |
| 373.15 | 7580.00 | 728.5 |
| 373.15 | 7930.00 | 728.9 |
| 373.15 | 8270.00 | 729.4 |
| 373.15 | 8620.00 | 729.9 |
| 373.15 | 8960.00 | 730.2 |
| 373.15 | 9310.00 | 730.6 |
| 373.15 | 9650.00 | 730.8 |
| 373.15 | 10000.00 | 731.0 |
| 373.15 | 10340.00 | 731.4 |
| 373.15 | 10690.00 | 731.6 |
| 373.15 | 11030.00 | 731.9 |
| 373.15 | 11380.00 | 732.1 |
| 393.15 | 340.00 | 710.0 |
| 393.15 | 690.00 | 710.3 |
| 393.15 | 1030.00 | 710.6 |
| 393.15 | 1380.00 | 710.9 |
| 393.15 | 1720.00 | 711.1 |
| 393.15 | 2070.00 | 711.4 |
| 393.15 | 2410.00 | 711.7 |
| 393.15 | 2760.00 | 712.0 |
| 393.15 | 3100.00 | 712.2 |
| 393.15 | 3450.00 | 712.3 |
| 393.15 | 3800.00 | 712.5 |
| 393.15 | 4140.00 | 712.8 |
| 393.15 | 4480.00 | 713.0 |
| 393.15 | 4830.00 | 713.3 |
| 393.15 | 5170.00 | 713.5 |
| 393.15 | 5510.00 | 713.8 |
| 393.15 | 5860.00 | 714.0 |
| 393.15 | 6200.00 | 714.3 |
| 393.15 | 6550.00 | 714.6 |
| 393.15 | 6890.00 | 714.9 |
| 393.15 | 7240.00 | 715.1 |
| 393.15 | 7580.00 | 715.3 |
| 393.15 | 7930.00 | 715.5 |
| 393.15 | 8270.00 | 715.8 |
| 393.15 | 8620.00 | 716.0 |
| 393.15 | 8960.00 | 716.3 |
| 393.15 | 9310.00 | 716.6 |
| 393.15 | 9650.00 | 716.8 |
| 393.15 | 10000.00 | 717.1 |
| 393.15 | 10340.00 | 717.4 |
| 393.15 | 10690.00 | 717.6 |
| 393.15 | 11030.00 | 717.9 |
| 393.15 | 11380.00 | 718.1 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [421.88; 585.67] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54069e+01 | |||
| Coefficient B | -4.97629e+03 | |||
| Coefficient C | -9.27430e+01 | |||
| Temperature range, min. | 421.88 | |||
| Temperature range, max. | 585.67 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| Pvap | 1.33 | kPa | 421.88 | Calculated Property |
| Pvap | 2.94 | kPa | 440.08 | Calculated Property |
| Pvap | 6.01 | kPa | 458.28 | Calculated Property |
| Pvap | 11.46 | kPa | 476.48 | Calculated Property |
| Pvap | 20.61 | kPa | 494.68 | Calculated Property |
| Pvap | 35.24 | kPa | 512.87 | Calculated Property |
| Pvap | 57.63 | kPa | 531.07 | Calculated Property |
| Pvap | 90.61 | kPa | 549.27 | Calculated Property |
| Pvap | 137.62 | kPa | 567.47 | Calculated Property |
| Pvap | 202.65 | kPa | 585.67 | Calculated Property |
| Pvap | [8.83e-05; 1413.13] | kPa | [291.32; 720.60] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.60137e+02 | |||
| Coefficient B | -1.55289e+04 | |||
| Coefficient C | -2.05917e+01 | |||
| Coefficient D | 8.01493e-06 | |||
| Temperature range, min. | 291.32 | |||
| Temperature range, max. | 720.60 | |||
|
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 400 600 | ||||
| Pvap | 8.83e-05 | kPa | 291.32 | Calculated Property |
| Pvap | 8.95e-03 | kPa | 339.02 | Calculated Property |
| Pvap | 0.22 | kPa | 386.72 | Calculated Property |
| Pvap | 2.29 | kPa | 434.41 | Calculated Property |
| Pvap | 13.07 | kPa | 482.11 | Calculated Property |
| Pvap | 50.12 | kPa | 529.81 | Calculated Property |
| Pvap | 145.97 | kPa | 577.51 | Calculated Property |
| Pvap | 350.91 | kPa | 625.20 | Calculated Property |
| Pvap | 737.67 | kPa | 672.90 | Calculated Property |
| Pvap | 1413.13 | kPa | 720.60 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexadecane.
Mixtures
- n-Hexane + Hexadecane
- Hexadecane + Tetradecane
- Hexadecane + 2,3-Pentanedione
- Hexadecane + Benzaldehyde
- Hexadecane + Octadecane
- Benzene + Hexadecane + Ethanol, 2-methoxy-
- Toluene + Hexadecane + Ethanol, 2-methoxy-
- p-Xylene + Hexadecane + Ethanol, 2-methoxy-
- Benzene + Acetonitrile + Hexadecane
- Toluene + Acetonitrile + Hexadecane
- Acetonitrile + p-Xylene + Hexadecane
- Hexadecane + Acetophenone
- Benzyl methyl ketone + Hexadecane
- Carbon dioxide + Hexadecane
- 1-Propanol + Hexadecane
- Hexadecane + 1-Butanol
- Hexadecane + Pentane, 3-methyl-
- Hexadecane + Butane, 2,2-dimethyl-
- Benzene + Hexadecane
- Isopropyl Alcohol + Hexadecane
Find more mixtures with Hexadecane.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
- Excess Volumes, Densities, Speeds of Sound, and Viscosities for the Binary Systems of 1-Octanol with Hexadecane and Squalane at (298.15, 303.15 and 308.15) K
- High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
- Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
- Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
- Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
- Measurement and correlation of liquid liquid equilibria for acetonitrile + n-alkane systems
- Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
- Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
- Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
- Ionic liquids on desulfurization of fuel oils
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- Separation of propylbenzene and n-alkanes from their mixtures using 4-methyl-N-butylpyridinium tetrafluoroborate as an ionic solvent at several temperatures
- Experimental measurements and equation of state modeling of liquid densities for long-chain n-alkanes at pressures to 265 MPa and temperatures to 523 K
- Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
- Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
- Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
- A modified continuous flow apparatus for gas solubility measurements at high pressure and temperature with camera system
- Experimental measurements and thermodynamic modeling of wax disappearance temperature for the binary systems n-C14H30 + n- C16H34, n-C16H34 + n-C18H38 and n-C11H24 + n-C18H38
- Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
- Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
- Speed of sound and thermodynamic properties of ternary liquid mixture octane + dodecane + hexadecane
- Extraction of nitrogen compounds from diesel fuel using imidazolium- and pyridinium- based ionic liquids: Experiments, COSMO-RS prediction and NRTL correlation
- Isobaric vapor-liquid equilibrium for the three binary systems of C14 - C16 n-alkane + methyl myristate at 5.00 kPa
- Measurements and prediction of ternary liquid-liquid equilibria for mixtures of IL + sulfur compound + hexadecane
- Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
- Evaluation of 1-ethyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate as solvents for extraction of alkylbenzenes from hexadecane at 313 and 333 K
- Liquid density measurements of cumene, tert-butylbenzene, and hexadecane over wide ranges of temperature and pressure
- A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
- Experimental measurement and thermodynamic modeling of phase equilibria of {CO2 + tetralin + n-alkanes (with n = 6, 16)} and its binary systems
- Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
- Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
- Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
- Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
- Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
- Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
- Density and speed of sound measurements of hexadecane
- Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
- Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
- Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
- Viscosity of n-hexadecane, n-octadecane and n-eicosane at pressures up to 243 MPa and temperatures up to 534 K
- Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
- Experimental measurement and prediction of (liquid + liquid + liquid) equilibrium for the system (n-hexadecane + water + triacetin)
- High pressure speed of sound and density of (decalin + n-decane), (decalin + n-hexadecane) and (n-decane + n-hexadecane) systems and thermodynamic modeling with PHCT equation of state
- Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
- Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
- Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
- Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
- Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
- Express thermo-gravimetric method for the vaporization enthalpies appraisal for very low volatile molecular and ionic compounds.
- Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
- Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
- Silver incorporated microencapsulation of n-hexadecane and noctadecane appropriate for dynamic thermal management in textiles
- Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
- Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
- Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
- Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
- Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
- Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
- Densities and Viscosities at 293.15 373.15 K, Speeds of Sound and Bulk Moduli at 293.15 333.15 K, Surface Tensions, and Flash Points of Binary Mixtures of n-Hexadecane and Alkylbenzenes at 0.1 MPa
- Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
- Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
- Synthesis and Physical and Thermodynamic Properties of Lactic Acid and Malic Acid-Based Natural Deep Eutectic Solvents
- Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
- Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
- Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
- Viscosities of Liquid Hexadecane at Temperatures between 323 K and 673 K and Pressures up to 4 MPa Measured Using a Dual-Capillary Viscometer
- Density and Volumetric Properties of Binary Mixtures of CO2 + Hexadecane from (303.2 to 473.2) K and Pressures up to 50.0 MPa
- Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
- Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
- Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
- Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
- Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
- Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
- Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
- Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
- Liquid-Liquid Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
- Liquid-Liquid Equilibria Measurements for Ternary System of Hexadecane + 1,3,5-Trimethylbenzene + N-Methyl-2-pyrrolidone
- High-Pressure Density Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
- Liquid-Liquid Equilibria for the Ternary System Water + Hexadecane + Propylene Glycol n-Propyl Ether
- Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
- Vapor Liquid Phase Equilibria and Physical Properties Measurements for Ternary Systems (Methane + Decane + Hexadecane)
- Temperature and Composition Effect on CO2 Miscibility by Interfacial Tension Measurement
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
- Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
- Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
- Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
- Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
- Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
- Binary Liquid-Liquid Equilibrium (LLE) for N-Methylformamide (NMF) + Hexadecane between (288.15 and 318.15) K and Ternary LLE for Systems of NMF + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
- Solubility of Carbon Dioxide in Water and Hexadecane: Experimental Measurement and Thermodynamic Modeling
- High-Pressure Viscosity Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
- Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
- Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
- (Liquid + Liquid) Equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T = 298.15 K
- Experimental Measurement and Thermodynamic Modeling for the Solubility of Methane in Water and Hexadecane
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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